Method for formulation of synthetic gas oils or additives for gas oil
    1.
    发明授权
    Method for formulation of synthetic gas oils or additives for gas oil 失效
    合成瓦斯油或瓦斯油添加剂的配制方法

    公开(公告)号:US07504548B2

    公开(公告)日:2009-03-17

    申请号:US10943896

    申请日:2004-09-20

    IPC分类号: C07C2/64 C10G35/00

    摘要: The invention relates to a method for formulation of a synthetic gas oil or an additive for gas oil in which an alkyl-aromatic compound or a mixture of alkyl-aromatic compounds is selected based on at least one parameter that is selected from the group that consists of the number of cycles of the aromatic core, the number of alkyl chains that are grafted to the aromatic cycle, the length of the alkyl chain or chains, the position of the aromatic cycle or cycles on the alkyl chain or chains of said alkyl-aromatic compound or compounds such that the cetane number of the synthetic gas oil or the additive for gas oil is greater than 30. The invention also relates to a process for the production of alkyl-aromatic compounds for use as a gas oil or additive.

    摘要翻译: 本发明涉及一种用于制备瓦斯油的合成瓦斯油或其添加剂的方法,其中烷基芳族化合物或烷基芳族化合物的混合物基于至少一个参数,该参数选自组成 的芳族核心的循环次数,接枝到芳香环的烷基链的数量,烷基链或链的长度,芳族环或在所述烷基链或烷基链的烷基链上的循环的位置, 芳族化合物或化合物,使得合成瓦斯油的十六烷值或瓦斯油的添加剂大于30.本发明还涉及用作瓦斯油或添加剂的烷基 - 芳族化合物的制备方法。

    Method for formulation of synthetic gas oils or additives for gas oil
    2.
    发明申请
    Method for formulation of synthetic gas oils or additives for gas oil 失效
    合成瓦斯油或瓦斯油添加剂的配制方法

    公开(公告)号:US20050065388A1

    公开(公告)日:2005-03-24

    申请号:US10943896

    申请日:2004-09-20

    摘要: The invention relates to a method for formulation of a synthetic gas oil or an additive for gas oil in which an alkyl-aromatic compound or a mixture of alkyl-aromatic compounds is selected based on at least one parameter that is selected from the group that consists of the number of cycles of the aromatic core, the number of alkyl chains that are grafted to the aromatic cycle, the length of the alkyl chain or chains, the position of the aromatic cycle or cycles on the alkyl chain or chains of said alkyl-aromatic compound or compounds such that the cetane number of the synthetic gas oil or the additive for gas oil is greater than 30. The invention also relates to a process for the production of alkyl-aromatic compounds for use as a gas oil or additive.

    摘要翻译: 本发明涉及一种用于制备瓦斯油的合成瓦斯油或其添加剂的方法,其中烷基芳族化合物或烷基芳族化合物的混合物基于至少一个参数,该参数选自组成 的芳族核心的循环次数,接枝到芳香环的烷基链的数量,烷基链或链的长度,芳族环或在所述烷基链或烷基链的烷基链上的循环的位置, 芳族化合物或化合物,使得合成瓦斯油的十六烷值或瓦斯油的添加剂大于30.本发明还涉及用作瓦斯油或添加剂的烷基 - 芳族化合物的制备方法。

    Process for oligomerizing olefins using a silica-alumina based catalyst
    3.
    发明授权
    Process for oligomerizing olefins using a silica-alumina based catalyst 有权
    使用二氧化硅 - 氧化铝基催化剂使烯烃低聚的方法

    公开(公告)号:US07572946B2

    公开(公告)日:2009-08-11

    申请号:US11182021

    申请日:2005-07-15

    IPC分类号: C07C2/08

    摘要: An olefin oligomerization process employs a particular silica-alumina catalyst which comprises a non zeolitic support based on silica-alumina containing a quantity of more than 5% by weight and 95% by weight or less of silica (SiO2) and has the following characteristics: a mean pore diameter, measured by mercury porosimetry, in the range 20 to 140 Å; a total pore volume, measured by mercury porosimetry, in the range 0.1 ml/g to 0.6 ml/g; a total pore volume, measured by nitrogen porosimetry, in the range 0.1 ml/g to 0.6 ml/g; a BET specific surface area in the range 100 to 550 m2/g; a pore volume, measured by mercury porosimetry, included in pores with a diameter of more than 140 Å, of less than 0.1 ml/g; a pore volume, measured by mercury porosimetry, included in pores with a diameter of more than 160 Å, of less than 0.1 ml/g; a pore volume, measured by mercury porosimetry, included in pores with a diameter of more than 200 Å, of less than 0.1 ml/g; a pore volume, measured by mercury porosimetry, included in pores with a diameter of more than 500 Å, of less than 0.1 ml/g; and an X ray diffraction diagram containing at least the principal characteristic peaks of at least one of the transition aluminas included in the group composed of alpha, rho, khi, eta, gamma, kappa, theta and delta aluminas.

    摘要翻译: 烯烃低聚方法使用特定的二氧化硅 - 氧化铝催化剂,其包含基于二氧化硅 - 氧化铝的非沸石载体,其含有大于5重量%且95重量%以下的二氧化硅(SiO 2),并具有以下特征: 通过水银孔率法测量的平均孔径在20至140埃的范围内; 通过水银孔率法测量的总孔体积在0.1ml / g至0.6ml / g的范围内; 通过氮气孔率法测量的总孔体积在0.1ml / g至0.6ml / g的范围内; 100-550m2 / g范围内的BET比表面积; 通过水银孔率法测定的孔体积,其直径大于140埃,小于0.1ml / g; 通过水银孔率法测量的孔体积,其直径大于160埃的孔隙小于0.1ml / g; 包含在直径大于200埃的孔中,通过水银孔率法测量的孔体积小于0.1ml / g; 通过水银孔率法测量的孔体积包含在直径大于500埃的小于0.1ml / g的孔中; 以及X射线衍射图,其至少包含由α,rho,khi,eta,γ,κ,θ和δ氧化铝组成的组中的至少一种过渡氧化铝的主要特征峰。

    Process for oligomerizing olefins using a silica-alumina based catalyst
    5.
    发明申请
    Process for oligomerizing olefins using a silica-alumina based catalyst 有权
    使用二氧化硅 - 氧化铝基催化剂使烯烃低聚的方法

    公开(公告)号:US20060063955A1

    公开(公告)日:2006-03-23

    申请号:US11182021

    申请日:2005-07-15

    IPC分类号: C07C2/00

    摘要: An olefin oligomerization process employs a particular silica-alumina catalyst which comprises a non zeolitic support based on silica-alumina containing a quantity of more than 5% by weight and 95% by weight or less of silica (SiO2) and has the following characteristics: a mean pore diameter, measured by mercury porosimetry, in the range 20 to 140 Å; a total pore volume, measured by mercury porosimetry, in the range 0.1 ml/g to 0.6 ml/g; a total pore volume, measured by nitrogen porosimetry, in the range 0.1 ml/g to 0.6 ml/g; a BET specific surface area in the range 100 to 550 m2/g; a pore volume, measured by mercury porosimetry, included in pores with a diameter of more than 140 Å, of less than 0.1 ml/g; a pore volume, measured by mercury porosimetry, included in pores with a diameter of more than 160 Å, of less than 0.1 ml/g; a pore volume, measured by mercury porosimetry, included in pores with a diameter of more than 200 Å, of less than 0.1 ml/g; a pore volume, measured by mercury porosimetry, included in pores with a diameter of more than 500 Å, of less than 0.1 ml/g; and an X ray diffraction diagram containing at least the principal characteristic peaks of at least one of the transition aluminas included in the group composed of alpha, rho, khi, eta, gamma, kappa, theta and delta aluminas.

    摘要翻译: 烯烃低聚方法使用特定的二氧化硅 - 氧化铝催化剂,其包含基于二氧化硅 - 氧化铝的非沸石载体,其含有大于5重量%和95重量%以下的二氧化硅(SiO 2/2) >),具有以下特征:通过水银孔率法测定的平均孔径在20〜140范围内; 通过水银孔率法测量的总孔体积在0.1ml / g至0.6ml / g的范围内; 通过氮气孔率法测量的总孔体积在0.1ml / g至0.6ml / g的范围内; 在100〜550m 2 / g范围内的BET比表面积; 通过水银孔率法测定的孔体积,其直径大于140埃,小于0.1ml / g; 包含在直径大于160埃的孔中,通过水银孔率法测量的孔体积小于0.1ml / g; 包含在直径大于200埃的孔中,通过水银孔率法测量的孔体积小于0.1ml / g; 通过水银孔率法测量的孔体积包含在直径大于500埃的小于0.1ml / g的孔中; 以及X射线衍射图,其至少包含由α,rho,khi,eta,γ,κ,θ和δ氧化铝组成的组中的至少一种过渡氧化铝的主要特征峰。

    Method for producing phenylalkanes using a combination of two catalysts
    6.
    发明授权
    Method for producing phenylalkanes using a combination of two catalysts 失效
    使用两种催化剂组合生产苯基烷烃的方法

    公开(公告)号:US07297826B2

    公开(公告)日:2007-11-20

    申请号:US10495773

    申请日:2002-11-05

    IPC分类号: C07C2/66

    摘要: A process is described for producing phenylalkanes by alkylating at least one aromatic compound using at least one linear olefin containing 9 to 16 carbon atoms per molecule. The alkylation reaction is carried out in the presence of at least two different catalysts used in at least two distinct reaction zones. The selectivity for a monoalkylated products of the catalyst contained in the first reaction zone is lower than that for the catalyst contained in the second reaction zone located downstream of the first in the direction movement of the fluids.

    摘要翻译: 描述了通过使用至少一种每分子含有9至16个碳原子的直链烯烃烷基化至少一种芳族化合物来制备苯基烷烃的方法。 烷基化反应在至少两个不同的反应区中使用的至少两种不同的催化剂存在下进行。 包含在第一反应区中的催化剂的单烷基化产物的选择性低于位于流体方向移动中第一个下游的第二反应区中的催化剂的选择性。

    Process for the valorization of a charge of hydrocarbons and for reducing the vapor pressure of said charge
    8.
    发明授权
    Process for the valorization of a charge of hydrocarbons and for reducing the vapor pressure of said charge 有权
    用于使碳氢化合物加压并且用于降低所述电荷的蒸汽压力的方法

    公开(公告)号:US07161052B2

    公开(公告)日:2007-01-09

    申请号:US10653426

    申请日:2003-09-03

    IPC分类号: C07C2/68 C07C2/04 C07C2/00

    CPC分类号: C10G29/205 C10G50/00

    摘要: A process is described for the valorization of a charge of hydrocarbons and for reducing the vapour pressure of said charge, comprising three steps: a step a) consisting of separating said charge of hydrocarbons into a fraction (O1) comprising essentially compounds containing 5 carbon atoms, including at least 2% by weight of pentenes, a step b) consisting of placing said fraction (O1) in contact with a cut of hydrocarbons (O2) at least partly comprising hydrocarbons having a number of carbon atoms between 6 and 10, including at least 2% by weight of olefins, and a step c) consisting of separating the effluents originating from step b) into a gasoline cut (α) the upper distillation point of which is less than 100° C. and a kerosene cut (β) having a distillation range between 100° C. and 300° C.

    摘要翻译: 描述了一种用于增加烃类和降低所述电荷的蒸气压的方法,包括三个步骤:步骤a)由将所述烃分离成基本上含有5个碳原子的化合物的馏分(O1)组成的步骤 ,包括至少2重量%的戊烯,步骤b)将所述馏分(O1)与至少部分包含6至10个碳原子的烃的馏分(O 2)接触,包括 至少2重量%的烯烃,以及步骤c),其通过将来自步骤b)的流出物分离成上馏分小于100℃的汽油馏分(α)和煤油切割(β ),其蒸馏范围为100℃至300℃。

    Process for the valorization of a charge of hydrocarbons and for reducing the vapour pressure of said charge
    10.
    发明申请
    Process for the valorization of a charge of hydrocarbons and for reducing the vapour pressure of said charge 有权
    用于使碳氢化合物加压并且用于降低所述电荷的蒸汽压力的方法

    公开(公告)号:US20050101821A1

    公开(公告)日:2005-05-12

    申请号:US10653426

    申请日:2003-09-03

    CPC分类号: C10G29/205 C10G50/00

    摘要: A process is described for the valorization of a charge of hydrocarbons and for reducing the vapour pressure of said charge, comprising three steps: a step a) consisting of separating said charge of hydrocarbons into a fraction (O1) comprising essentially compounds containing 5 carbon atoms, including at least 2% by weight of pentenes, a step b) consisting of placing said fraction (O1) in contact with a cut of hydrocarbons (O2) at least partly comprising hydrocarbons having a number of carbon atoms between 6 and 10, including at least 2% by weight of olefins, and a step c) consisting of separating the effluents originating from step b) into a gasoline cut (α) the upper distillation point of which is less than 100° C. and a kerosene cut (β) having a distillation range between 100° C. and 300° C.

    摘要翻译: 描述了一种用于增加烃类和降低所述电荷的蒸气压的方法,包括三个步骤:步骤a)由将所述烃分离成基本上含有5个碳原子的化合物的馏分(O1)组成的步骤 ,包括至少2重量%的戊烯,步骤b)将所述馏分(O1)与至少部分包含6至10个碳原子的烃的馏分(O 2)接触,包括 至少2重量%的烯烃,以及步骤c),其通过将来自步骤b)的流出物分离成上馏分小于100℃的汽油馏分(α)和煤油切割(β ),其蒸馏范围为100℃至300℃。